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JPH0429401B2 - - Google Patents
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JPH0429401B2 - - Google Patents

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Publication number
JPH0429401B2
JPH0429401B2 JP60286912A JP28691285A JPH0429401B2 JP H0429401 B2 JPH0429401 B2 JP H0429401B2 JP 60286912 A JP60286912 A JP 60286912A JP 28691285 A JP28691285 A JP 28691285A JP H0429401 B2 JPH0429401 B2 JP H0429401B2
Authority
JP
Japan
Prior art keywords
particles
air
particle size
liquid tank
liquid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP60286912A
Other languages
Japanese (ja)
Other versions
JPS62149331A (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP28691285A priority Critical patent/JPS62149331A/en
Publication of JPS62149331A publication Critical patent/JPS62149331A/en
Publication of JPH0429401B2 publication Critical patent/JPH0429401B2/ja
Granted legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Glanulating (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、クりーンルームや微小孔フイルター
の性能試験あるいは磁気テープや熱交換器壁の塗
付材料、燃料触媒等、極めて広い応用範囲を有す
る微粒子の分野において、任意の粒怪を持つ粒子
を発生させる装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is applicable to fine particles which have an extremely wide range of applications such as performance testing of clean rooms and microporous filters, coating materials for magnetic tapes and heat exchanger walls, and fuel catalysts. The present invention relates to a device for generating particles having arbitrary particle size in the field of.

従来の技術 微粒子及び超微粒子(数10オングストローム〜
100μm)の発生及び調整方法に関し、さまざま
な研究開発が進められており、例えば昭和60年3
月10日、日本ビジネスリポート株式会社発行の技
術予測シリーズ第5巻・新素材編には、「超微粒
子の現況と将来展望」及び「フアインセラミツク
スの展望」と題する論文が掲載されている。この
中にも掲載されているように、従来の微粒子の調
整方法では、ある濃度の微粒子を含む液をいれた
混合器の中にN2,He,Ar,H2等のキヤリヤー
ガスを導入し液中でガスをバブリングさせること
によつて微粒子を飛散させている。ところが、こ
の方法であると生成される微粒子の粒径のばらつ
きが極端に大きくなり、さらに数量的にも安定し
た粒子数を発生させることが不可能であつた。こ
のため粒径及び粒子数のばらつきに起因する様々
な欠点を生じていた。
Conventional technology Fine particles and ultrafine particles (several tens of angstroms ~
100μm) generation and adjustment methods, various research and development efforts are underway; for example, in March 1985,
On April 10th, Volume 5 of the Technology Forecast Series, New Materials Edition, published by Japan Business Report Co., Ltd., included papers titled ``Current Status and Future Prospects of Ultrafine Particles'' and ``Prospects of Fine Ceramics.'' As described in this publication, the conventional method for preparing fine particles involves introducing a carrier gas such as N 2 , He, Ar, H 2 , etc. into a mixer containing a liquid containing fine particles at a certain concentration. Fine particles are dispersed by bubbling gas inside. However, with this method, the variation in particle size of the fine particles produced becomes extremely large, and furthermore, it is impossible to generate a quantitatively stable number of particles. This has resulted in various drawbacks due to variations in particle size and number of particles.

発明が解決しようとする問題点 本発明の目的は、任意の粒径を持つ粒子を空気
中に長時間安定して発生させることができる装置
を提供することにある。
Problems to be Solved by the Invention An object of the present invention is to provide an apparatus that can stably generate particles having any particle size in the air for a long period of time.

本発明の他の目的は、粒子の数量を長時間安定
して発生させることができる装置を提供すること
にある。
Another object of the present invention is to provide an apparatus that can stably generate a large number of particles over a long period of time.

問題点を解決するための手段とその作用 本発明の前述した目的は、霧化すべき液体と粒
子を形成し得る物質とを入れる液槽の一部に取付
けた超音波振動子と、該液槽の上部に設けたガス
を送り込む第1の送風口と、該液槽の上部から上
方に伸びる吹き出し管と、該吹き出し管の途中に
設けたガスを送りこむ第2の送風口と、第1の送
風口からの送風量を調節する第1のバルブ機構
と、第2の送風口からの送風量を調節する第2の
バルブ機構とを備えた任意粒径粒子の発生装置に
よつて達成される。
Means for Solving the Problems and Their Effects The above objects of the present invention are to provide an ultrasonic transducer attached to a part of a liquid tank containing a liquid to be atomized and a substance capable of forming particles; a first air outlet provided at the top of the liquid tank for sending gas, a blowing pipe extending upward from the top of the liquid tank, a second blowing port provided in the middle of the blowing pipe for sending gas, and a first air blowing port. This is achieved by a generator for generating particles of arbitrary particle size, which includes a first valve mechanism that adjusts the amount of air blown from the opening, and a second valve mechanism that adjusts the amount of air blown from the second air outlet.

すなわち本発明は超音波霧化装置を利用する。
この超音波霧化装置内に向けて第1の送風口から
送り込むガスの量と、吹き出し管の途中に向けて
第2の送風口から送り込むガスの量との配分を変
化させることによつて、空気中に安定した粒径の
粒子及び数量的にも安定した粒子を発生させるこ
とが出来る。さらに必要に応じて液濃度を変化さ
せることにより、任意の粒径及び数量の粒子を発
生させることが可能になる。
That is, the present invention utilizes an ultrasonic atomization device.
By changing the distribution of the amount of gas sent into the ultrasonic atomizer from the first air outlet and the amount of gas sent from the second air outlet towards the middle of the blowout pipe, It is possible to generate particles with a stable particle size and quantitatively stable particles in the air. Furthermore, by changing the liquid concentration as necessary, it becomes possible to generate particles of arbitrary particle size and number.

すなわち、第1のバルブ機構を制御して第1の
送風口から液槽内へと送り込む空気の量を調節す
ることにより、液槽から吹き出し管へと運ばれる
粒子の径を制御することができる。なぜならば、
液面から発生したミストの粒径にはある程度のば
らつきがあるが、粒径の大きなものは沈降速度が
大きいから、一定風量以下では吹き出し管へと運
ばれることがなく液面へと落下する。これによ
り、吹き出し管へと向かう粒子の径を一定以下に
抑えることが可能になる。また、第2のバルブ機
構を制御して第2の送風口から出口へと向かう風
量を調整することにより、出口における空気とミ
ストとの混合比すなわち粒子濃度を制御すること
ができる。さらに、液槽内の溶液の濃度を変化さ
せることにより、液面から発生したミストの乾燥
後の粒子径を制御することもできる。
That is, by controlling the first valve mechanism to adjust the amount of air sent into the liquid tank from the first air outlet, it is possible to control the diameter of the particles carried from the liquid tank to the blowout pipe. . because,
The particle size of the mist generated from the liquid surface varies to some extent, but larger particles have a higher settling speed, so below a certain air volume, the mist falls to the liquid surface without being carried to the blowout pipe. This makes it possible to suppress the diameter of particles heading toward the blowout pipe to a certain level or less. Furthermore, by controlling the second valve mechanism to adjust the amount of air flowing from the second air outlet to the outlet, it is possible to control the mixing ratio of air and mist at the outlet, that is, the particle concentration. Furthermore, by changing the concentration of the solution in the liquid tank, it is also possible to control the particle size of the mist generated from the liquid surface after drying.

安定した粒径を得ることができる理由として
は、液中にある濃度で微粒子、高分子材、塩化物
等が一様に分布又は溶け込んでいるため、超音波
によつて発生したミスト内に含まれる分量もほぼ
一様な量となること、ミストが空気中に運ばれる
時、溶剤(溶媒)のみが蒸発し、微粒子、高分子
材、塩化物等が空気中において凝集する分量が一
様なため、発生した粒子の粒径も一様になること
等が考えられる。
The reason why we are able to obtain a stable particle size is because fine particles, polymer materials, chlorides, etc. are uniformly distributed or dissolved in the liquid at a certain concentration. When the mist is carried into the air, only the solvent (solvent) evaporates, and the amount of fine particles, polymer materials, chlorides, etc. that aggregate in the air is uniform. Therefore, it is thought that the particle size of the generated particles becomes uniform.

送風口から送り込むガスとしては、空気のほか
各種の気体を利用することができるが、各送風口
において湿り気のない乾燥ガスであることが望ま
しい。
Although various gases other than air can be used as the gas sent through the ventilation ports, it is preferable that each ventilation port uses dry gas without moisture.

以下、添付図面の実施例を参照しながら本発明
をさらに説明する。
The invention will now be further explained with reference to embodiments of the accompanying drawings.

実施例 第1図は本発明による粒子発生装置の好適な実
施例を表わしており、液槽10の中に霧化すべき
液体として水が溶剤として入れられ、霧化すべき
粒子を形成し得る物質として粒計0.091μmのラテ
ツクス球が混入されている。液槽10の底面には
超音波振動子として厚電振動子12が取付けら
れ、駆動回路14から交流信号を受けて振動し超
音波振動を発生させることにより液体を振動さ
せ、表面から水及びラテツクス球を霧状に飛散さ
せるようになつている。液槽10の上部側壁には
乾燥空気を送り込むための第1の送風口16が設
けられ、液槽10の上面には上方に伸びる吹き出
し管20が取付けられている。さらに吹き出し管
20の途中には乾燥空気を送り込むための第2の
送風口18が設けられ、吹き出し管20はこの位
置から水平方向に伸びて出口22から所定の粒径
に凝集したラテツクス粒子を放出するようになつ
ている。送風口16,18にはエアポンプ24か
らそれぞれバルブ26,28を介して乾燥空気が
供給される。バルブ26,28は制御機構30、
例えば電気式・電子式・空気式の自動制御装置か
らの信号を受けて流量調整を行ない、第1及び第
2の送風口へ供給する空気量を調節しその配分比
を変化させる。
Embodiment FIG. 1 represents a preferred embodiment of the particle generator according to the invention, in which water is placed as a solvent in the liquid tank 10 as the liquid to be atomized and as a substance capable of forming the particles to be atomized. Latex balls with a particle size of 0.091 μm are mixed. A thick electric vibrator 12 is attached to the bottom of the liquid tank 10 as an ultrasonic vibrator, and receives an AC signal from a drive circuit 14 and vibrates to generate ultrasonic vibrations, thereby vibrating the liquid and removing water and latex from the surface. It is designed to scatter the balls in a mist. A first air outlet 16 for feeding dry air is provided on the upper side wall of the liquid tank 10, and a blowing pipe 20 extending upward is attached to the upper surface of the liquid tank 10. Further, a second blowing port 18 for feeding dry air is provided in the middle of the blowing pipe 20, and the blowing pipe 20 extends horizontally from this position and releases latex particles aggregated to a predetermined particle size from an outlet 22. I'm starting to do that. Dry air is supplied to the ventilation ports 16 and 18 from an air pump 24 via valves 26 and 28, respectively. The valves 26 and 28 are controlled by a control mechanism 30;
For example, the flow rate is adjusted in response to a signal from an electric, electronic, or pneumatic automatic control device, and the amount of air supplied to the first and second ventilation ports is adjusted to change the distribution ratio.

第2図は、第1図の装置によつて発生させられ
る粒子の粒径が均一になることを説明する原理図
である。まずAの状態において水溶液中にラテツ
クス球が一様に分散している。Bの状態では超音
波振動によつて水面から発生したミストの中にラ
テツクス球が含まれている。Cの状態では乾燥ガ
スによつてミスト中の溶液すなわち水だけが蒸発
し、ラテツクス球が粒径Xに凝集した状態で残さ
れる。Dの状態になると粒径Xに凝集した状態の
ラテツクス球だけが残され、水は完全に蒸発して
気化し見えなくなる。かくして出口からは粒径が
均一になつた粒子(微粒子集合体)が放出され
る。
FIG. 2 is a principle diagram illustrating the fact that the particles generated by the apparatus shown in FIG. 1 have a uniform particle size. First, in state A, latex spheres are uniformly dispersed in an aqueous solution. In state B, latex spheres are included in the mist generated from the water surface by ultrasonic vibration. In state C, only the solution in the mist, that is, water, is evaporated by the drying gas, leaving latex spheres aggregated to a particle size of X. In state D, only latex spheres coagulated to particle size X remain, and the water completely evaporates and becomes invisible. In this way, particles (fine particle aggregate) with uniform particle sizes are discharged from the outlet.

実験例 第3図は、粒径0.091μmのラテツクス球を水に
混入させた液を用いて本発明の方法により粒子を
発生させ、3時間にわたつて発生粒子数(粒径
0.091μm}を測定しその経時変化を求めたグラフ
である。縦軸の発生粒子濃度は、1立方フイート
(0.0283立方メートル)当りの個数を対数値スケ
ールで表わしている。このグラフから、発生粒子
濃度が3時間にわたつてほぼ均一であり、極めて
安定した粒子の発生が得られることが判明した。
Experimental Example Figure 3 shows the number of particles generated (particle size
0.091 μm} is measured and its change over time is determined. The concentration of generated particles on the vertical axis is expressed in the number per cubic foot (0.0283 cubic meter) on a logarithmic scale. From this graph, it was found that the concentration of generated particles was almost uniform over 3 hours, and extremely stable particle generation was obtained.

第4図は、ラテツクス球の代りにNaClを水に
溶かした水溶液を用いて本発明の方法により粒子
を発生させ、空気量の配分を一定にしてNaCl濃
度を0.1%と1%とに変化させて発生粒子数と粒
径との関係を求めたグラフである。このグラフで
は粒径のピークが明白に表われており、ほぼ均一
な粒径の粒子が得られることが実証された。また
NaClの濃度を変化させることにより任意の粒径
を得ることが出来ることも判明した。
Figure 4 shows that particles are generated by the method of the present invention using an aqueous solution of NaCl dissolved in water instead of latex spheres, and the NaCl concentration is varied between 0.1% and 1% while keeping the air volume distribution constant. This is a graph showing the relationship between the number of particles generated and the particle size. In this graph, the particle size peak is clearly visible, demonstrating that particles of approximately uniform size can be obtained. Also
It was also found that any particle size could be obtained by changing the concentration of NaCl.

上記実施例及び実験例では溶剤(溶媒)が水の
場合について記載したが、溶剤は水に限定される
ことなく、溶質の種類により、例えばアルコー
ル、エーテル、石油エーテル、ベンゼン、酢酸エ
チル、クロロホルムなどを用いることが出来る。
In the above Examples and Experimental Examples, the case where the solvent (solvent) is water is described, but the solvent is not limited to water, and may be used depending on the type of solute, such as alcohol, ether, petroleum ether, benzene, ethyl acetate, chloroform, etc. can be used.

発明の効果 以上詳細に説明した如く、本発明の装置によれ
ば任意の粒径を持つ粒子を空気中に長時間安定し
て発生させることができ、さらに粒子の数量を長
時間安定させることもでき、クリーンルームや微
小孔フイルターの性能試験がより正確に行なえる
ようになる他、磁気テープや熱交換器の性能が向
上する等、その作用効果には極めて顕著なものが
ある。
Effects of the Invention As explained in detail above, according to the apparatus of the present invention, particles with any particle size can be stably generated in the air for a long time, and the number of particles can also be stabilized for a long time. Its effects are extremely remarkable, such as enabling more accurate performance testing of clean rooms and microporous filters, as well as improving the performance of magnetic tapes and heat exchangers.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明による粒子発生装置の概略断面
図、第2図は本発明の原理を表わす概略図、第3
図は発生粒子数の経時変化を表わすグラフ、第4
図は溶液の濃度を変化させて発生粒子数と粒径と
の関係を求めたグラフである。 10……液槽、12……超音波振動子、14…
…駆動回路、16,18……送風口、20……吹
き出し管、22……出口、24……ポンプ、2
6,28……バルブ。
FIG. 1 is a schematic sectional view of a particle generator according to the present invention, FIG. 2 is a schematic diagram showing the principle of the present invention, and FIG.
The figure is a graph showing the change in the number of generated particles over time.
The figure is a graph showing the relationship between the number of particles generated and the particle size by varying the concentration of the solution. 10...Liquid tank, 12...Ultrasonic vibrator, 14...
...Drive circuit, 16, 18...Blower port, 20...Blowout pipe, 22...Outlet, 24...Pump, 2
6,28...Valve.

Claims (1)

【特許請求の範囲】 1 霧化すべき液体と粒子を形成し得る物質とを
入れる液槽の一部に取付けた超音波振動子と、該
液槽の上部に設けたガスを送り込む第1の送風口
と、該液槽の上部から上方に伸びる吹き出し管
と、該吹き出し管の途中に設けたガスを送り込む
第2の送風口と、第1の送風口からの送風量を調
整する第1のバルブ機構と、第2の送風口からの
送風量を調整する第2のバルブ機構とを備えるこ
とを特徴とする任意粒径粒子の発生装置。 2 前記各送風口から送り込まれるガスは湿り気
のない乾燥空気である特許請求の範囲第1項記載
の装置。
[Claims] 1. An ultrasonic vibrator attached to a part of a liquid tank containing a liquid to be atomized and a substance capable of forming particles, and a first air blower installed above the liquid tank to send gas. an outlet, a blowout pipe extending upward from the top of the liquid tank, a second blowout port provided in the middle of the blowout tube to send gas, and a first valve that adjusts the amount of air blown from the first blowout port. 1. A generator for generating particles of any particle size, comprising: a mechanism; and a second valve mechanism that adjusts the amount of air blown from a second air outlet. 2. The device according to claim 1, wherein the gas sent from each of the air outlets is dry air without moisture.
JP28691285A 1985-12-21 1985-12-21 Generator for generating particles of arbitrary size Granted JPS62149331A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28691285A JPS62149331A (en) 1985-12-21 1985-12-21 Generator for generating particles of arbitrary size

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28691285A JPS62149331A (en) 1985-12-21 1985-12-21 Generator for generating particles of arbitrary size

Publications (2)

Publication Number Publication Date
JPS62149331A JPS62149331A (en) 1987-07-03
JPH0429401B2 true JPH0429401B2 (en) 1992-05-18

Family

ID=17710593

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28691285A Granted JPS62149331A (en) 1985-12-21 1985-12-21 Generator for generating particles of arbitrary size

Country Status (1)

Country Link
JP (1) JPS62149331A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2637139B2 (en) * 1988-02-26 1997-08-06 株式会社東芝 Manufacturing method of liquid crystal element
WO2007070957A1 (en) * 2005-12-21 2007-06-28 Monash University Process and apparatus for generating particles
JP2021090928A (en) * 2019-12-12 2021-06-17 昭和電工マテリアルズ株式会社 Extraction method and extraction device
US20220186280A1 (en) * 2020-12-15 2022-06-16 Sanko Tekstil Isletmeleri San. Ve Tic. A.S. Method for testing bacterial filtration efficacy of fabrics

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5043059A (en) * 1973-08-20 1975-04-18
JPS5285074A (en) * 1976-01-09 1977-07-15 Hitachi Ltd Granulation

Also Published As

Publication number Publication date
JPS62149331A (en) 1987-07-03

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